CN203068506U - Anthracite rotary cement kiln combustor head component - Google Patents

Anthracite rotary cement kiln combustor head component Download PDF

Info

Publication number
CN203068506U
CN203068506U CN 201220650325 CN201220650325U CN203068506U CN 203068506 U CN203068506 U CN 203068506U CN 201220650325 CN201220650325 CN 201220650325 CN 201220650325 U CN201220650325 U CN 201220650325U CN 203068506 U CN203068506 U CN 203068506U
Authority
CN
China
Prior art keywords
head
cyclone
injector
eddy flow
connector
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
CN 201220650325
Other languages
Chinese (zh)
Inventor
赵亮
窦海建
张凯
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
TIANJIN SINOMA ENGINEERING RESEARCH CENTER Co Ltd
Tianjin Cement Industry Design and Research Institute Co Ltd
Original Assignee
TIANJIN SINOMA ENGINEERING RESEARCH CENTER Co Ltd
Tianjin Cement Industry Design and Research Institute Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by TIANJIN SINOMA ENGINEERING RESEARCH CENTER Co Ltd, Tianjin Cement Industry Design and Research Institute Co Ltd filed Critical TIANJIN SINOMA ENGINEERING RESEARCH CENTER Co Ltd
Priority to CN 201220650325 priority Critical patent/CN203068506U/en
Application granted granted Critical
Publication of CN203068506U publication Critical patent/CN203068506U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Landscapes

  • Furnace Details (AREA)
  • Muffle Furnaces And Rotary Kilns (AREA)

Abstract

The utility model discloses an anthracite rotary cement kiln combustor head component. A head big outer barrel and a middle big outer barrel are connected and sleeved outside a head ejector and an ejector connecting piece to form an axial flow air channel. The ejector and the ejector connecting piece are connected and sleeved outside a head outer swirler and an outer swirler connecting piece to form an outer swirling flow air channel. The head outer swirler and the outer swirler connecting piece are connected and sleeved outside a head pulverized coal outlet and a middle pulverized coal outlet to form a coal air channel. The head pulverized coal outlet and the middle pulverized coal outlet are connected and sleeved outside a head inner swirler and an inner swirler connecting piece to form an inner swirling flow air channel. Swirling flow grooves I are formed in the head outer swirler, and the rotation direction of the swirling grooves I is identical to the rotation direction of a rotary kiln. Swirling flow grooves II are formed in the head inner swirler, and the rotation direction of the swirling flow grooves II is opposite to the rotation direction of the rotary kiln. Calcining effect of anthracite can be greatly improved in the process of cement clinker production.

Description

A kind of anthracite cement rotary kiln burner head parts
Technical field
The utility model relates to cement industry and makes field, particularly a kind of anthracite cement rotary kiln burner head parts.
Background technology
Coal burner is the core heat construction equipment of cement plant calcination of cement clinker, and its serviceability directly influences stable, the technical performance of rotary kiln of firing system and the yield and quality of clinker.For reducing cost, adapt to market competition, increasing cement plant brings into use the colm of low volatile and anthracite to act as a fuel, and anthracitic combustibility is poor, low, the more difficult after-flame of volatile matter.The result of use of burner depends primarily on performance and the structure of its head assembly, in the current manufacture of cement of making fuel with anthracite, the coal burner excuse parts that often occurs selecting for use designs unreasonable, cause system problems such as the preceding temperature of kiln is on the low side, coal dust after-burning, kiln caudal knot circle, influence ordinary production.
Summary of the invention
The utility model provides a kind of simple in structure, handling safety, the anthracite cement rotary kiln burner head parts that investment is little and operation rate is high for solving the technical problem that exists in the known technology.
The technical scheme that the utility model is taked for the technical problem that exists in the solution known technology is: a kind of anthracite cement rotary kiln burner head parts comprises cyclone and interior cyclone connector in the big urceolus of head, the big urceolus in middle part, head injector, injector connector, the outer cyclone of head, outer cyclone connector, head discharge, middle part discharge, the head;
The big urceolus of described head and described middle part coaxial connection of big urceolus, and be sleeved on the outside of described head injector and described injector connector, form the axial flow air channel, described head injector and described coaxial connection of injector connector, and be sleeved on the outside of the outer cyclone of described head and described outer cyclone connector, form outer swirling wind channel, the outer cyclone of described head and described outer coaxial connection of cyclone connector, and be sleeved on the outside of described head discharge and described middle part discharge, form coal wind duct, described head discharge and described middle part coaxial connection of discharge, and be sleeved on cyclone in the described head and described in the outside of cyclone connector, in the eddy flow air channel in forming, described head cyclone with described in the cyclone connector is coaxial is connected;
The head of cyclone is provided with the outer outside described head, the outer of the outer cyclone of described head and the interior circle of described head injector are tightly connected, the outer of the outer cyclone of described head is provided with a plurality of eddy flow groove I of offering along described outer swirling wind channel direction, the eddy flow angle of described eddy flow groove I is the 18-22 degree, and the direction of rotation of described eddy flow groove I is identical with the rotary kiln rotation direction;
The head of cyclone is provided with the outer in described head, the outer of cyclone and the interior circle of described head discharge are tightly connected in the described head, the outer of cyclone is provided with a plurality of eddy flow groove II of offering along described interior eddy flow air channel in the described head, the eddy flow angle of described eddy flow groove II is the 40-60 degree, and the direction of rotation of described eddy flow groove II is opposite with the rotary kiln rotation direction.
Head at described head injector is provided with the outer, and the interior circle of the outer of described head injector and the big urceolus of described head is tightly connected, and the outer of described head injector is provided with 16 through holes of offering along described axial flow air channel.
Advantage and the good effect that the utlity model has are:
1) inverse double-rotation stream wind setting, peripheral eddy flow wind and kiln turn to identical, strengthen the radial diffusion of coal dust, avoid coal dust to enter material too early simultaneously, and interior eddy flow wind strengthens coal dust with outer eddy flow wind reciprocation and spreads increase coal dust and gas contact area;
2) uniform 16 hole axial flow wind can make in the circumferential area peripheral gas is entrainmented the power maximum, and 16 hole axial flow wind hole counts had both enlarged the diameter of single hole, reduced the interference between the Kong Yukong simultaneously, strengthen comprehensive volume suction degree;
3) a wind ratio is low, economizes on coal obviously, to reducing system's hear rate certain effect is arranged;
4) the bispin flow structure can enlarge the combustion zone, reduces temperature peak, can effectively reduce generation and the discharging of NOx;
5) adjusting is nimble quick, and maintenance is convenient;
6) low wearing and tearing, the life-span is long.
In sum, the utility model has solved original burner and entrainmented problems such as secondary wind energy power deficiency, calcining heat are low, coal dust after-burning, kiln caudal knot circle when using anthracite, has significantly promoted anthracitic calcining effect in the clinker production process.
Description of drawings
Fig. 1 is side view of the present utility model;
Fig. 2 is the A-A cutaway view of Fig. 1;
Fig. 3 is outer eddy flow emitter construction schematic diagram;
Fig. 4 is interior eddy flow emitter construction schematic diagram.
Among the figure: the 1st, the big urceolus of head, the 2nd, the big urceolus, the 3rd in middle part, head injector, the 4th, injector connector, the 5th, the outer cyclone, the 6th of head, outer cyclone connector, the 7th, head discharge, the 8th, middle part discharge, the 9th, cyclone, the 10th in the head, interior cyclone connector.
The specific embodiment
For further understanding summary of the invention of the present utility model, characteristics and effect, exemplify following examples now, and conjunction with figs. is described in detail as follows:
See also Fig. 1~Fig. 4, a kind of anthracite cement rotary kiln burner head parts, comprise the big urceolus 1 of head, the big urceolus 2 in middle part, head injector 3, injector connector 4, the outer cyclone 5 of head, outer cyclone connector 6, head discharge 7, middle part discharge 8, cyclone 9 and interior cyclone connector 10 in the head, the big urceolus 1 of head and big 2 coaxial connections of urceolus of middle part, and be sleeved on the outside of head injector 3 and injector connector 4, form the axial flow air channel, head injector 3 and 4 coaxial connections of injector connector, and be sleeved on the outside of the outer cyclone 5 of head and outer cyclone connector 6, form outer swirling wind channel, the outer cyclone 5 of head and the outer cyclone connector 6 coaxial outsides that are connected and are sleeved on head discharge 7 and middle part discharge 8, form coal wind duct, head discharge 7 and 8 coaxial connections of middle part discharge, and be sleeved on the outside of cyclone 9 and interior cyclone connector 10 in the head, cyclone 9 and interior 10 coaxial connections of cyclone connector in the eddy flow air channel in forming, head.The head of cyclone 5 is provided with the outer outside head, the outer of the outer cyclone 5 of head and the interior circle of head injector 3 are tightly connected, the outer of the outer cyclone 5 of head is provided with a plurality of eddy flow groove I of offering along the outer swirling wind channel direction, the eddy flow angle of eddy flow groove I is the 18-22 degree, and the direction of rotation of eddy flow groove I is identical with the rotary kiln rotation direction.The head of cyclone 9 is provided with the outer in head, the outer of cyclone 9 and the interior circle of head discharge 7 are tightly connected in the head, the outer of cyclone 9 is provided with the eddy flow groove II that the eddy flow air channel is offered in a plurality of edges in the head, the eddy flow angle of eddy flow groove II is the 40-60 degree, and the direction of rotation of eddy flow groove II is opposite with the rotary kiln rotation direction.
Head at head injector 3 is provided with the outer, and the interior circle of the big urceolus 1 of the outer of head injector 3 and head is tightly connected, and the outer of head injector 3 is provided with 16 through holes of offering along the axial flow air channel.
Said burner utilizes the maximization of axial flow wind passage loose structure to the effect of entrainmenting of combustion air by the reasonable coupling design to axial flow air channel, outer swirling wind channel, coal wind duct, four main channels, interior eddy flow air channel, accelerates anthracitic ignition.Utilize outer eddy flow wind to increase the radial diffusion of coal dust, and the interior eddy flow wind of topmost acting in opposition strengthens the diffusion of coal dust greatly, the combustion zone coal dust is more evenly distributed, accelerate anthracite combustion, promote burn-off rate, the flame of having avoided occurring in the anthracite combustion is spun out, and calcining is not enough, problem such as ring formation behind the kiln.Anthracitic even burning can also reduce temperature peak, effectively reduces generation and the discharging of NOx, reaches the effect of energy-saving and emission-reduction.
The exclusive structure of the utility model has solved the problem that calcined anthracite in the present manufacture of cement exists, function admirable, regulate nimble quick, maintenance is convenient, wear and tear low, the life-span is long.
Its operation principle is: adopt high axial wind and inverse double-rotation stream structure combining of entrainmenting ability, and by reasonably coupling design, flow air in each air channel is spouting with different speed and angle, strengthen mixing of coal dust and high temperature secondary wind greatly, avoided dramatically because the incomplete system problem that brings of anthracite combustion.
Although by reference to the accompanying drawings preferred embodiment of the present utility model is described above; but the utility model is not limited to the above-mentioned specific embodiment; the above-mentioned specific embodiment only is schematic; be not restrictive; those of ordinary skill in the art is under enlightenment of the present utility model; not breaking away under the scope situation that the utility model aim and claim protect, can also make a lot of forms, these all belong within the protection domain of the present utility model.

Claims (2)

1. anthracite cement rotary kiln burner head parts, it is characterized in that, comprise cyclone and interior cyclone connector in the big urceolus of head, the big urceolus in middle part, head injector, injector connector, the outer cyclone of head, outer cyclone connector, head discharge, middle part discharge, the head;
The big urceolus of described head and described middle part coaxial connection of big urceolus, and be sleeved on the outside of described head injector and described injector connector, form the axial flow air channel, described head injector and described coaxial connection of injector connector, and be sleeved on the outside of the outer cyclone of described head and described outer cyclone connector, form outer swirling wind channel, the outer cyclone of described head and described outer coaxial connection of cyclone connector, and be sleeved on the outside of described head discharge and described middle part discharge, form coal wind duct, described head discharge and described middle part coaxial connection of discharge, and be sleeved on cyclone in the described head and described in the outside of cyclone connector, in the eddy flow air channel in forming, described head cyclone with described in the cyclone connector is coaxial is connected;
The head of cyclone is provided with the outer outside described head, the outer of the outer cyclone of described head and the interior circle of described head injector are tightly connected, the outer of the outer cyclone of described head is provided with a plurality of eddy flow groove I of offering along described outer swirling wind channel direction, the eddy flow angle of described eddy flow groove I is the 18-22 degree, and the direction of rotation of described eddy flow groove I is identical with the rotary kiln rotation direction;
The head of cyclone is provided with the outer in described head, the outer of cyclone and the interior circle of described head discharge are tightly connected in the described head, the outer of cyclone is provided with a plurality of eddy flow groove II of offering along described interior eddy flow air channel in the described head, the eddy flow angle of described eddy flow groove II is the 40-60 degree, and the direction of rotation of described eddy flow groove II is opposite with the rotary kiln rotation direction.
2. according to the described anthracite cement rotary kiln of claim 1 burner head parts, it is characterized in that, head at described head injector is provided with the outer, the interior circle of the outer of described head injector and the big urceolus of described head is tightly connected, and the outer of described head injector is provided with 16 through holes of offering along described axial flow air channel.
CN 201220650325 2012-11-29 2012-11-29 Anthracite rotary cement kiln combustor head component Expired - Lifetime CN203068506U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201220650325 CN203068506U (en) 2012-11-29 2012-11-29 Anthracite rotary cement kiln combustor head component

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201220650325 CN203068506U (en) 2012-11-29 2012-11-29 Anthracite rotary cement kiln combustor head component

Publications (1)

Publication Number Publication Date
CN203068506U true CN203068506U (en) 2013-07-17

Family

ID=48767285

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201220650325 Expired - Lifetime CN203068506U (en) 2012-11-29 2012-11-29 Anthracite rotary cement kiln combustor head component

Country Status (1)

Country Link
CN (1) CN203068506U (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106885237A (en) * 2017-02-23 2017-06-23 河南汇金智能装备有限公司 Burner
CN108758629A (en) * 2018-07-10 2018-11-06 东方电气集团东方锅炉股份有限公司 low nitrogen oxide gas burner
CN109059534A (en) * 2018-06-12 2018-12-21 湖北锋焰机电科技有限公司 A kind of adjustable energy-efficient rotary kiln burner
CN113464933A (en) * 2021-07-02 2021-10-01 合肥水泥研究设计院有限公司 Swirler with gradually changed spiral angle
CN114674146A (en) * 2022-03-18 2022-06-28 天津水泥工业设计研究院有限公司 Intelligent control system and control method for rotary cement kiln burner
CN114674146B (en) * 2022-03-18 2024-06-07 天津水泥工业设计研究院有限公司 Intelligent control system and control method for cement rotary kiln burner

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106885237A (en) * 2017-02-23 2017-06-23 河南汇金智能装备有限公司 Burner
CN106885237B (en) * 2017-02-23 2023-09-22 河南汇金智能装备有限公司 Burner with a burner body
CN109059534A (en) * 2018-06-12 2018-12-21 湖北锋焰机电科技有限公司 A kind of adjustable energy-efficient rotary kiln burner
CN109059534B (en) * 2018-06-12 2024-02-23 湖北锋焰机电科技有限公司 Adjustable high-efficiency energy-saving rotary kiln burner
CN108758629A (en) * 2018-07-10 2018-11-06 东方电气集团东方锅炉股份有限公司 low nitrogen oxide gas burner
CN108758629B (en) * 2018-07-10 2024-04-12 东方电气集团东方锅炉股份有限公司 Low-oxynitride gas burner
CN113464933A (en) * 2021-07-02 2021-10-01 合肥水泥研究设计院有限公司 Swirler with gradually changed spiral angle
CN114674146A (en) * 2022-03-18 2022-06-28 天津水泥工业设计研究院有限公司 Intelligent control system and control method for rotary cement kiln burner
CN114674146B (en) * 2022-03-18 2024-06-07 天津水泥工业设计研究院有限公司 Intelligent control system and control method for cement rotary kiln burner

Similar Documents

Publication Publication Date Title
CN100538177C (en) Double passage ejection energy-saving burner
CN103615717A (en) Novel oxygen enrichment tiny-oil ignition and ultralow load stable-combustion combustor
CN203068506U (en) Anthracite rotary cement kiln combustor head component
CN107606613A (en) The low nitrogen rotational flow gas-fired combustor of flue gas recirculation built in gas-air Accurate Classification
CN109931605B (en) Multistage air distribution radial outer thick and inner thin cyclone burner
CN102537959B (en) Rotational flow and direct current combined gas burner
CN202792006U (en) Head assembly of high-thrust and double-rotational-flow coal dust burner
CN207527582U (en) The low nitrogen rotational flow gas-fired combustor of flue gas recirculation built in gas-air Accurate Classification
CN201885229U (en) Low-emission high-power sectionalized combustion gas burner
CN206145669U (en) Swirling flow pulverized coal burner
CN102633452B (en) Out-of-kiln pre-decomposition system for cement clinker
CN209840083U (en) Multistage air distribution radial outer thick inner thin cyclone burner
CN109973994B (en) Low-nitrogen burner
CN109099425B (en) Flue gas inner loop ultralow nitrogen combustor
CN208418734U (en) A kind of low-NOx combustor for natural gas and coal dust
CN115264500A (en) Double-cyclone burner for cement clinker production
CN210004390U (en) oxygen-enriched flat flame burner
CN205155958U (en) Be suitable for low NOx combustor of various low heat values / low pressure gas
CN209484602U (en) A kind of interior super low NO of circulation of flue gas
CN201233008Y (en) Coal powder burner
CN204388126U (en) A kind of gas-turbine combustion chamber blade Inlet Swirl nozzle
CN103411215A (en) Multi-directional jet-type cyclone pulverized coal burner
CN203731402U (en) A dual-air-regulating pulverized coal burner for an industrial pulverized coal boiler
CN209876911U (en) Large coal powder concentration ratio delay mixed type rotational flow coal powder burner
CN106196042B (en) A kind of strong swirl jet burner

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CX01 Expiry of patent term

Granted publication date: 20130717

CX01 Expiry of patent term